Method for calibrating a device for measuring the concentration of creatinine

ABSTRACT

A method of calibrating a device for measuring the concentration of creatinine using one or more calibration solutions, the method comprising: receiving concentrations at an initial time of creatine, Cr, and/or creatinine, Crn, of the one or more calibration solutions; receiving outputs of the measuring device at the end time; calculating the concentration of Cr and/or Crn in the calibration solutions at an end time using a temperature model, wherein the temperature model indicates changes in temperature of the calibration solutions from the initial time to the end time; and determining a relationship between the outputs of the measuring device and the calculated concentrations of Cr and/or Crn.

FIELD OF THE INVENTION

The invention relates to methods for calibrating creatinine measuringdevices, and calibration solutions for use in those methods.

BACKGROUND

Techniques for measuring the concentration of creatinine (Crn) andcreatine (Cr) are useful in medicine, for example in monitoring renaldisease. The concentration of Cr (cCr) and the concentration of Crn(cCrn) in an aqueous solution can be determined by amperometricmeasurement. Two sensors are used in the measurement of cCrn: the Crea Asensor, which detects Cr; and the Crea B sensor, which detects both Crand Crn. The cCrn is based on the difference between the Crea A and CreaB sensor measurements.

In order to determine cCrn in unknown samples with sufficient accuracy,the Crea A and Crea B sensors must be calibrated regularly in order todetermine their actual sensitivities. The sensors can be calibratedusing two aqueous calibration solutions of known cCrn and cCr. However,a problem with such calibration solutions is that cCr and cCrn are notfixed. Rather, when in aqueous solution, Crn can be converted into Crand vice versa by water hydrolysis and elimination respectively, asindicated by the double arrow in the reaction equation in Scheme 1,where T is the temperature at which the reaction occurs and k₁ and k₂are the rate constants for the hydrolysis and elimination reactionsrespectively.

After a sufficient period of time at a constant temperature the mixturewill reach a dynamic equilibrium in which cCr and cCrn are constant.However, changes to the temperature of the solution will shift theequilibrium ratio, and therefore the cCr and cCrn will change.

A calibration solution having known cCr and cCrn in equilibrium ratios,can be generated by adding the enzyme creatinine amidohydrolase (CA) toa solution of known sum concentration of Cr and Crn, and then allow thatsolution to equilibrate by maintaining the solution at a specifictemperature for about one hour. The CA facilitates equilibration. Onceequilibrium is reached at a given temperature, the cCr and cCrn can bedetermined simply by reference to the known equilibrium constants at thegiven temperature.

WO 2005/052596 discloses a reference solution for quality control on amedical analyser and a kit for holding the reference solution. The kitcomprises a container with a first and a second compartment, wherein thefirst and the second compartment may be separated by a thin wall, whichmay be broken upon exertion of manual pressure, which will cause theliquids of the first and second compartments to mix. The firstcompartment comprises a buffer, and the second compartment comprises twochemical compounds and a catalyst. When the two compunds, the catalystand the buffer is mixed, a thermodynamic equilibrium is reached morerapidly allowing the solution to be used as quality control referencesolution within hours, when conditioned at 25° C., whereas the solutionwould otherwise have to be conditioned for much longer, if no catalystwas used.

For sensors responding linearly to changes in both cCr and cCrn it isrequired that the chosen compositions of the two calibration solutionsresult in a linearly independent equation system, i.e.,cCr_(CalX)=m·cCr_(CalY) and cCrn_(CalX)=n·cCrn_(CalY) with m ≠ n isrequired. Hence, only one of the calibration solutions can contain Crand Crn at their equilibrium concentrations unless stored at twodifferent temperatures. However, the best sensor calibration may beobtained by using one solution of essentially pure Cr and one solutionof essentially pure Crn.

Calibration solutions having known cCr and cCrn in non-equilibriumratios can be prepared by dissolving a known quantity of dry powdercontaining known quantities of Cr and Crn in a known volume of water, orother aqueous medium.

Typically, the calibration solution is kept at between 15° C. to 32° C.,which allows for accurate calculations for solutions less than 14 daysold, even when approximating this to be at a constant temperature.Therefore, existing methods are sufficiently accurate to enable thecalculation of cCr and cCrn for calibration solutions having a shortusage period (i.e. t_(age)<14 days).

Another alternative is to produce an acidic creatinine solution, this isthermodynamically stable and can thus be maintained during storage. Thissolution can then be mixed with a buffer-solution immediately before useto obtain a calibration solution of essentially pure Crn with a known pHand cCrn, such as disclosed in US 2004/0072277. A problem with thisapproach is that it is difficult to produce a homogeneous mixture if thetwo solutions are contained in sealed airtight pouches. Additionally,the mixing process will also require pumping means if automatic mixingis required and/or if the pouches are part of a closed system, such as acassette based solution pack. Furthermore, it is not advisable to letthe solution pass through the sensor chamber, since the CA enzyme mayleak out of the creatinine sensors, for example, and into the solutionthereby destroying the non-equilibrium conditions. To prevent that couldnecessitate a separate channel for liquid transport.

In both cases, having a 14 day time limit for the accuracy of thecalibration solution is disadvantageous in that frequent replacement isrequired, which is uneconomical and inconvenient for the end user.Furthermore, the short usage period may be reduced even further becausethe end user may have to wait several days for the solution to bedelivered from the manufacturer. Alternatively the end user may beobliged to prepare the calibration solution at the point of use (e.g.hospital), which introduces additional work for the end user as well asthe risk of inaccuracies, for example in weighing the Cr and Crn powderand measuring the volume of solvent or by uneven mixing. An unmet needexists for an approach enabling the use of calibration solutions havinga t_(age)>14 days.

SUMMARY OF THE INVENTION

In a first aspect of the present invention, the applicant makesavailable a method of calibrating a device for measuring theconcentration of creatinine using one or more calibration solutions, themethod comprising: receiving concentrations at an initial time ofcreatine, Cr, and/or creatinine, Crn, of the one or more calibrationsolutions; receiving outputs of the measuring device at the end time;calculating the concentration of Cr and/or Crn in the calibrationsolutions at an end time using a temperature model, wherein thetemperature model indicates changes in temperature of the calibrationsolutions from the initial time to the end time; and determining arelationship between the outputs of the measuring device and thecalculated concentrations of Cr and/or Crn.

By using a temperature model of the calibration solutions, it ispossible to accurately calibrate the sensors even when the initialconcentrations of the solutions have been measured over 14 days beforecalibration. The customer is not restricted to utilise the calibrationsolutions within a short time span after receiving the calibrationsolutions, as a temperature model allows the customer to store thesolutions at a range of temperatures, while still providing accuratecalibrations.

In some example embodiments the measuring device includes a sensor formeasuring creatine in one or more of the calibration solutions.

In some example embodiments the measuring device includes a sensor formeasuring creatinine in one or more of the calibration solutions.

In some example embodiments the measuring device includes a sensor formeasuring creatine and creatinine in one or more of the calibrationsolutions.

In some example embodiments the measuring device is an amperometricmeasuring device.

In some example embodiments, the method further comprises determiningthe temperature model by receiving measurements of the changes intemperature of the calibration solutions from a temperature probe fromthe initial time to the end time. By using a temperature probe tomeasure changes in temperature of the calibration solutions over thetime period between the initial time and the end time, it is possible toaccurately calculate the end concentrations of the calibrationsolutions.

In some example embodiments, the received measurements are recordedmeasurements.

In some example embodiments said determining the temperature modelcomprises calibrating the received measurements of the changes intemperature with a second temperature probe.

In some example embodiments the determining a relationship between themeasuring device outputs and the calculated concentrations of Cr and Crncomprises calculating sensor sensitivities of the measuring devices.

In some example embodiments the method further comprises receivingtemperature measurements after the end time and updating the calculatedsensitivities of the measuring devices using the temperaturemeasurements received after the end time.

In some example embodiments the end time is greater than 14 days afterthe initial time.

According to another aspect of the present invention, a computerreadable medium is provided comprising instructions which when executedby one or more processors of an electronic device, cause the electronicdevice to operate in accordance with any of the aforementioned methods.

According to another aspect of the present invention, an electronicdevice is provided comprising: one or more processors; and memorycomprising instructions which when executed by one or more of theprocessors cause the electronic device to operate in accordance with anyof the aforementioned methods.

According to another aspect of the present invention, a package isprovided comprising one or more calibration solutions, the package beingsuitable for use with any of the aforementioned methods oraforementioned electronic devices.

In some example embodiments, the package further comprises an indicationof the initial time and the concentrations at the initial time ofcreatine (Cr) and/or creatinine (Crn) of the one or more calibrationsolutions.

In some example embodiments, the package further comprises a temperatureprobe for measuring the temperatures of the creatinine solutions fromthe initial time to the end time, and memory for storing the measuredtemperatures.

BRIEF DESCRIPTIONS OF DRAWINGS

Examples of the present proposed apparatus will now be described indetail with reference to the accompanying drawings, in which:

FIG. 1 is a schematic diagram of an example of an amperometric measuringsystem;

FIG. 2 is a graph showing the temperature variation of calibrationsolutions and a corresponding two-temperature model estimating thetemperature variation;

FIG. 3 is a flow chart showing the derivation of the proposed method;

FIG. 4 is a flow chart outlining the steps of the proposed method;

FIG. 5 is a series of graphs comparing the concentrations in thecalibration solutions with the concentrations calculated in accordancewith an example embodiment of the proposed method; and

FIG. 6 is a series of graphs comparing the concentrations in thecalibration solutions with the concentrations calculated in accordancewith a further example embodiment of the proposed method.

DETAILED DISCLOSURE

Reference will now be made to FIG. 1 which is a schematic diagram of athree-electrode amperometric measuring system 101. An amperometricmeasuring system may have at least two electrodes: a working electrode(WE) 110 and a combined counter and reference electrode (CE/RE). For thethree-electrode amperometric measuring system 101, the functions of theCE/RE electrode are split into two separate electrodes: the referenceelectrode (RE) 111 and the counter electrode (CE) 112. The exampleamperometric measuring system 101 also includes an ammeter 120, avoltmeter 121 and a voltage source 122 and the electrolyte solution 140.

The WE 110 is a positively charged electrode where an oxidation reactionoccurs. The RE 111 is typically made of Ag/AgCl and is able to maintaina stable potential, especially if no current runs through it, thus theneed for a CE 112 for passing the current from the WE 110 back to theelectrolyte solution 140. The electrolyte solution 140/sample provides acurrent path between the three electrodes. The membrane 130 selectivelyconverts the analyte to a substance that selectively is allowed to passthrough from the sample 150. The voltage source 122 applies thenecessary potential for maintaining the desired reduction or oxidationreaction, this is controlled by the voltmeter 121. The ammeter 120measures the resulting current flowing through the electrical circuit.

The amperometric measuring system shown in FIG. 1 is an illustrativeexample, and several other implementations are envisioned. For example,the amperometric measuring system could be a two electrode system asmentioned above.

The magnitude of an electrical current flowing through the electrodechain is proportional to the concentration of the substance beingoxidized (or reduced) at the WE 110. Ideally, when knowing theproportionality constant relating the electrical current to aconcentration, the concentration in any given sample can be obtained bymeasuring the electrical current generated by that particular sample.

To illustrate the measuring process in an amperometric measuring system,we assume that: The sample 150 contains species B which, in the membrane130, is selectively converted to species A, which can be oxidized at theWE 110 (WE) to A⁺; and the electrolyte 140 contains species X which isreduced at the CE 112 (cathode) to X⁻. We assume also that the membrane130 allows only species A to pass from the sample into the electrolytesolution 140.

As an appropriate potential is applied across the electrodes, A isoxidized at the WE 110 according to the following reaction:

A→A⁺+e⁻

The oxidation of A produces a flow of electrons. To complete theelectrical circuit a reduction reaction where electrons are consumed isnecessary. Therefore species X is reduced at the CE 112 according to thefollowing reaction:

X+e⁻→X⁻

The magnitude of the current flowing through the circuit is proportionalto the concentration of the analyte being oxidized. The analyser cantherefore automatically calculate the concentration of the analyte inthe sample given species X is in excess.

The term sensor refers to a complete amperometric measuring system, asshown in FIG. 1 excluding the sample 150.

Crn is not stable in aqueous solutions, e.g. blood, where it isreversibly converted into Cr (see Scheme 1). To measure cCrn, thepresent invention utilizes a two-sensor system where one sensor (Crea A)detects Cr only, and the other sensor (Crea B) detects both Cr and Crn.By means of a difference measurement it is possible to obtain the cCrnvalue.

The sensor is protected by a multilayer membrane 130 consisting of atleast three functional layers, namely the outer membrane layer permeableto Crn and Cr; the middle enzyme layer, and the inner membrane layerpermeable to H₂O₂.

Crn and Cr molecules diffuse across the outer membrane layer. Theenzymes creatinine amidohydrolase, creatine amidinohydrolase andsarcosine oxidase are immobilized between the inner and outer membranelayers. The Crea A sensor contains only creatine amidinohydrolase andsarcosine oxidase, and so detects only Cr. In the Crea A sensor, theenzymatic cascade changes Cr as follows:

Creatine+H₂O→sarcosine+urea (creatine amidinohydrolase)

Sarcosine+H₂O+O₂→glycine+formaldehyde+H₂O₂ (sarcosine oxidase)

The Crea B sensor contains all three enzymes creatinine amidohydrolase,creatine amidinohydrolase and sarcosine oxidase, and so detects both Crnand Cr. In the enzymatic cascade Crn/Cr changes as follows:

Creatinine+H₂O

creatine (creatinine amidohydrolase)

Creatine+H₂O→sarcosine+urea (creatine amidinohydrolase)

Sarcosine+H₂O+O₂→glycine+formaldehyde+H₂O₂ (sarcosine oxidase)

For both the Crea A and the Crea B sensors the enzyme reactions lead toidentical end-products, one of which is H₂O₂ that can diffuse across theinner membrane layer to the WE 110 (preferably platinum). By applying asufficiently high electrical potential to the electrode chains of theCrea A and Crea B sensors, H₂O₂ can be oxidized at the WE 110:

H₂O₂→2H⁺+O₂+2e⁻

To complete the electrical circuit, electrons are consumed in reductionreactions at the CE 112 thereby maintaining a charge balance between theWE 110 and the CE 112.

The oxidation of H₂O₂ produces an electrical current (I) proportional tothe amount of H₂O₂, which in turn is directly related to the amount ofCr for the Crea A and the amount of Cr and Crn for the Crea B sensorsaccording to the sensor response models:

I ^(A) =S _(Cr) ^(A) ·cCr   Equation 1

I ^(B) =S _(Cr) ^(B) ·cCr+S _(Crn) ^(B) ·cCrn   Equation 2

Where I^(A) and I^(B) are the electrical currents produced at the Crea Aand Crea B sensors respectively; S_(Cr) ^(A) and S_(Cr) ^(B) are thesensitivity constants relating current (I) to Cr concentration in theCrea A and Crea B sensors respectively and S_(Crn) ^(B) is thesensitivity constant relating current (I) to Crn concentration in theCrea B sensor.

The proportionality constants, S, relating currents to concentrationsare typically referred to as sensitivities. The constants are determinedby calibrating the sensors. The current (signal) of each sensor ismeasured by ammeters 120 in the analyser. If sensor sensitivities S areknown, the unknown Crn concentration in a given sample is readilydetermined from the equations above.

The changes in cCr and cCrn relative to the last known values of cCr andcCrn can be calculated based on reaction rate equations and rateconstants described by the Arrhenius equation. To make the calculationit is necessary to know the period of time elapsed since the cCr andcCrn was last known (t_(age)), and the temperature experienced by thesolution during that period.

One way of making accurate estimations of cCr and cCrn when thecalibration solution has experienced a range of temperatures, is torecord the changes in temperature since the last concentrationmeasurements. For example, when the calibration solutions are shipped,the calibration solution packs may include a temperature measurementdevice and a means for recording the changes in temperature.

One example implementation would include a temperature probe thatrecords the temperature of the solutions at regular intervals intocomputer memory, so that when the solutions need to be calibrated, thememory can be accessed to determine the temperatures experienced. Thecombination of a temperature probe and memory for recording the recordedtemperatures may be referred to herein as a temperature logger.

Knowing the historic changes in temperature, it is possible toaccurately calculate the changes in concentration from the initialconcentrations recorded to a calculated concentration at the time ofcalibration. For example, it is possible to calculate the change in cCrnand cCr over time based on the reaction rate equations and the rateconstants described by the Arrhenius equation, and applied to therecorded temperatures over time.

As each solution pack would require a temperature logger, to reduce thecosts it may be beneficial to use a low-cost temperature probe. While alow-cost temperature probe may lead to inaccurate temperaturemeasurements, the temperature probe may be calibrated with a moreaccurate temperature probe. This calibration may involve comparingmeasurements by the low-cost and reference temperature probe for onetemperature or over a range of temperatures to determine if there is adifference between the measurements. If a difference is determined, therecorded temperatures in the memory may be offset by this difference.The offsetting of recorded temperatures may be applied to readingsalready recorded, or may be applied to all subsequent recordings oftemperature.

Temperature loggers packaged with solution packs can be used to providean accurate measurement of temperature changes while the solution packis being stored and transported, and eventually can be used to helpcalibrate sensors. Once the calibration solutions have reached theirdestinations, the sensors can been calibrated using the accompanyingtemperature loggers, and the temperature may then be continued to bemonitored by a more accurate temperature logger to ensure that thesensor sensitivities are kept up to date. The more accurate temperaturelogger may be part of a measurement station or may be part of apermanent instalment of the end user.

Surprisingly it has been found that in one embodiment calculating theconversions in the calibrators using a temperature logger with atemperature offset from the real temperature, and a thermal exposurethat does not quite resemble the temperature profile experienced by thecalibration solutions still can provide an acceptable estimate of the Crand Crn concentrations in the calibrators. Therefore, such calibrationof the temperature probes may not be required, and the low-costtemperature probes may be used. Using a temperature logger as anestimate of the exact temperature profile can provide sufficient datafor estimating the Cr and Crn concentrations in the calibrators.

While using one or more temperature measurement devices and recordingthe measurements can lead to very accurate calculations for endconcentrations, it may be advantageous to calculate similarly accurateresults without the use of temperature probes or memory in order toreduce the costs of each pack of calibration solutions. One such methodinvolves using temperature models to estimate the changes intemperatures experienced.

FIG. 2 is a graph showing an example temperature profile of calibrationsolutions and a corresponding two-temperature model estimating thetemperature variation. The true temperature profile 210 shows the actualtemperature variation from an initial time 230 (t=0) to an end time 232(t=t_(age)). In this example, the temperature starts at a low 4° C. foran initial period of 4 days in storage at the manufacturer 211. When thecalibrations solutions are transported, the temperature rises to ahigher temperature of 31° C. for a period of roughly 14 days 212. Aftertransporting 212 the calibration solutions, they are stored at a lowtemperature (roughly 5° C.) with the customer 213 for a period ofroughly 76 days. In this example, the customer takes the calibrationsolutions out of storage in order to use them over a period of 14 days214, during which time, the calibration solutions are kept at a highertemperature of roughly 20° C.

While the end user will be aware of the temperature of the calibrationsolution if the user prepared it themselves by combining an aqueousmedium of known temperature and Cr and Crn powder, the user will not beaware of the temperature profile from the point of production up tousage if prepared by the manufacturer. As shown in FIG. 2, the truetemperature profile 210 can be very complicated, with large temperaturefluctuations over a long period of time. In the past, such temperaturefluctuations have made it difficult to accurately calculate theconcentration levels of the calibration solutions.

The applicant has surprisingly identified that although a temperatureprofile is not necessarily known by the customer, the complextemperature profile can be modelled by a much simpler temperature model.An example temperature model, a two-temperature model 220, is indicatedin FIG. 2. The complex temperature profile is modelled as having a lowtemperature of T₁=2° C. 241 for a first time period 221 from an initialtime t=0 230 to an intermediate time t=t₁ 231, and then having a hightemperature of T₂=32° C. 242 for a period 222 from the intermediate timet=t₁ 231 to an end time t=t_(age) 232. While the two-temperature model220 in FIG. 2 does not exactly match the true temperature profile 210,it provides a functional estimation of the changes in temperature.

The value of t₁ can be optimised to compensate for any discrepanciesbetween the true temperature profile 210 and the two-temperature model220. For example, although the final increase in temperature in the truetemperature profile 210 occurs at about 107 days, the correspondingincrease in temperature of the two-temperature model 220 occurs at anearlier time t=t₁=95 days. This earlier time for t₁ is earlier than theactual increase in temperature to compensate for the large increase intemperature during the initial transport phase 212. Similarly, if thetemperature values T₁ and T₂ are chosen to be too high or too low, thevalue of t₁ can be adjusted to compensate for this as well.

The true temperature profile can be simplified to a multiple-temperaturemodel as the pattern of storage, transport and usage conditions for thecreatinine/creatine solutions follow similar patterns. Table 1 shows theestimated time and temperature ranges for an example calibrationsolution supporting cCrn measurements.

TABLE 1 Max. time [days] Temperatures [° C.] Storage at manufacturer 562-8 Transport from manufacturer 14  2-32 to customer Storage at customer108 (~3½ months) 2-8 Usage 14 15-32

Other multiple-temperature models could be used. For example, atemperature model with three or more temperatures may be used. Ratherthan discrete step changes in temperature, progressive cooling andheating of the temperatures could be incorporated into the model usingsimple exponential functions, or fluctuations could be incorporated intothe model using sinusoidal functions, for example.

In the example embodiment provided, a two-temperature model is used asit provides a simple illustration of the proposed solution. In thisexample embodiment, the following calibrators, Cal2 and Cal3, are usedfor calibrating the Crea A and Crea B sensors:

TABLE 2 At time: t_(production) Cal2 Cal3 cCr [μM] 0 500 cCrn [μM] 500 0Sensor Crea B Crea A and Crea B

In addition to the Cr and Crn, calibrators Cal2 and Cal3 may alsocontain buffers, salts, preservatives and detergents. For the purposesof the proposed method, the concentrations of only Cr and Crn in thecalibrators will be reviewed.

In the example embodiment presented herein, the concentrations of bothCr and Crn are being determined through the use of two calibrationsolutions and two sensors. However, it is envisioned that the proposedmethod may be used to calculate only the Cr concentrations or only theCrn concentrations. If concentrations of just one substance isdetermined (Cr or Crn), then only one specific sensor (Cr or Crn) andtwo calibration solutions are needed.

As shown in Scheme 1, Crn can be converted into Cr and vice versa bywater hydrolysis and elimination in a reversible reaction. Thisreversible conversion reaction starts immediately when either of the twospecies are dissolved in water and it will continue with a higher ratein one direction until the system reaches thermodynamic equilibrium,i.e., until Crn and Cr reach their mutual equilibrium concentrations(cX_(eq)) according to the equilibrium constant (K_(eq)(T)) of thisreaction:

$\begin{matrix}{{K_{eq}(T)} = {\frac{{cCr}_{eq}(T)}{{cCrn}_{eq}(T)} = {\frac{k_{1}(T)}{k_{2}(T)}.}}} & {{Equation}\mspace{14mu} 3}\end{matrix}$

The equilibrium constant can also be expressed in terms of rateconstants k₁(T) and k₂(T) for the forward and backward reactions (theindividual arrows) involved in the conversion reaction in Scheme 1. Therate constants are temperature dependent, but are not necessarilyequally dependent. Therefore, the equilibrium constant K_(eq)(T) of theconversion reaction (and hence the equilibrium concentration of Crn andCr) will also be temperature dependent.

The temperature dependency of the rate constants is dictated by theArrhenius-equation:

$\begin{matrix}{{{k_{i}( T_{t} )} = {{A_{i} \cdot {\exp ( \frac{\beta_{i}}{T_{t}} )}} = {\exp ( {\alpha_{i} + \frac{\beta_{i}}{T_{t}}} )}}},{{{where}\mspace{14mu} \alpha_{i}} = {\ln \; A_{i}}}} & {{Equation}\mspace{14mu} 4}\end{matrix}$

The subscript on the temperature T is here used as a short hand notationto indicate that it may be a function of time t. α_(i) and β_(i) are therelevant Arrhenius parameters for the reaction in consideration, whichare known with a very high degree of accuracy.

The above reactions are spontaneously taking place in calibrator Cal2and Cal3 from the moment when Cr and/or Crn are added during theproduction process. Therefore, the actual concentrations of Cr and Crnin the calibrators in a solution pack strongly depend on the time passedsince production and on the temperature profile T_(protiie)(t)experienced by the individual solution pack during that time span. Table2 shows the changes in concentration of Cr and Crn in Cal2 and Cal3 as afunction of time and the temperature profile:

TABLE 3 At time: t > t_(production) Cal2 Cal3 cCr [μM] ΔcCrn_(Cal2)(t,T_(profile)(t)) 500-ΔcCr_(Cal3)(t, T_(profile)(t)) cCrn [μM]500-ΔcCrn_(Cal2)(t, T_(profile)(t)) ΔcCr_(Cal3)(t, T_(profile)(t))

In Table 3, ΔcCrn_(Cal2) is the change in the Crn concentration in Cal2up to time t due to its one to one conversion into Cr; and ΔcCr_(Cal3)is the change in the Cr concentration in Cal3 up to time t due to itsone to one conversion into Crn.

The concentration change (dcCrn) of cCrn during an infinitesimal timespan (dt) obeys the following differential equation, also known as therate equation:

$\begin{matrix}{{\frac{dcCrn}{dt} = {{{k_{2}( T_{t} )} \cdot {cCr}} - {{k_{1}( T_{t} )} \cdot {cCrn}}}},} & {{Equation}\mspace{14mu} 5}\end{matrix}$

Combining the reaction rate equations (Equation 5), with the Arrheniusequations (Equation 4) and the two-temperature model, provides theanalytic expressions cCr_(Cal#) ^(model)(t₁) and cCrn_(Cal#)^(model)(t₁), which are respectively the Cr and Crn concentrations incalibrator “Cal#” as functions of the time t₁ spent at the initialtemperature T₁, typically the lower temperature.

If each of the true temperature profile (T_(t)=T_(profile)(t)); therelevant Arrhenius-parameters (α_(i) and β_(i)) for the above reaction;and the starting concentrations cCr_(Cal#) ⁰ and cCrn_(Cal#) ⁰ of Cr andCrn in calibrator Cal# at time t=0, are known, then very accurateestimates of the true Cr and Crn concentrations in that calibrator atany time afterwards can be obtained by integration of the rate equation.

The true temperature profile experienced by the calibration solutionsduring storage, transport, storage at the customer, and usage, may notbe known by the end user if no record of temperature variation isavailable. Although the exact temperature profile may be unknown, thereare several variables independent of one another that can be measured toreveal details of the conditions. Therefore, in order to obtain asufficiently accurate estimate of the unknown true temperature profilewe utilize all available degrees-of-freedom (DOFs) in the cCrn measuringsystem, that are not utilized for other purposes, e.g., for calibratingthe Crea A and Crea B sensors.

The measurements with the Crea A and Crea B sensors on the twocalibrations solutions Cal2 and Cal3 result in 4 sensors signals, i.e. 4available DOFs. According to Table 2 and its supporting text, 3 out ofthe 4 available DOFs are allocated for sensor calibration purposes,which leave one unused DOF in surplus: the Crea A signal on Cal2. Thissingle DOF can be utilized to determine the value of an “unknown” entityin the same manner as the other 3 DOFs will be utilized for determiningthe 3 “unknown” sensor sensitivities.

FIG. 3 is a flow chart showing the step-by-step derivation for theproposed method of determining analyte levels in the calibrators andsubsequently calibrating the sensors.

As discussed above, the rate equation 310 (Equation 5) is combined withthe Arrhenius equation 311 (Equation 4) and the temperature model 320.To choose an appropriate temperature model, one needs to be aware of thegeneral pattern of temperature fluctuations that are to be expected.Table 1 provides an example of this general pattern as it indicates thedifferent conditions (storage at production, transport, storage atcustomer, and usage) that the calibrations solutions may undergo. Thetable also shows the temperature ranges that the calibration solutionsare expected to experience, and it indicates what time periods thesesolutions are expected to remain at these conditions.

The chosen temperature model may have an initial temperature (T₁) at aninitial time (t_(production) or t=0), an end temperature (T₂) at thetime of calibration (t_(age)), and an intermediate (t₁) at which thetemperature changes from the initial to the end temperature. While theinitial time and end time will be known, and the initial temperature andend temperature are either known or estimated, the intermediate time t₁may not be known at all. In such a scenario, the available DOF can beused to determine this intermediate time t₁.

The skilled person would look at the data available, and construct atemperature model accordingly. Where there is one available DOF, thetemperature model would be constructed so that there is only oneunknown, such as intermediate time t₁. Where there is more than oneavailable DOF, a temperature model can be constructed with as manyunknowns as there are available DOFs.

In the embodiment described above, the available DOF is used todetermine the variable parameter t₁, in a temperature model comprisingtwo known (or estimated) temperatures and the time t₁ at which thetemperature changes between the two. Another possible use of theavailable DOF is to determine an average conversion temperature beingused throughout the whole timespan t_(age)−t_(production), in atemperature model comprising a single unknown temperature as thevariable parameter.

In the example presented herewith, the true temperature profileT_(profile)(t) can be modelled by a two-temperature model, which dependson initial and end temperatures T₁ and T₂, end time t_(age) andintermediate time t₁ (and implicitly initial time t₀=0). Given thegeneral pattern identified, the two temperature can modelled as a simplestep change from an initial temperature to an end temperature at theintermediate time t₁. This model can be represented as:

$\begin{matrix}{{T_{profile}^{model}( {{t;T_{1}},T_{2},t_{1},t_{age}} )} = \{ \begin{matrix}{T_{1},} & {0 \leq t \leq t_{1}} \\{T_{2},} & {t_{1} < t \leq t_{age}}\end{matrix} } & {{Equation}\mspace{14mu} 6}\end{matrix}$

Temperatures T₁ and T₂ can, in principle, be chosen arbitrarily.However, to ensure that the model can encompass all possible temperaturescenarios, the temperatures T₁ and T₂ may be set to match the expectedtemperature ranges. Using the expected patterns set out in Table 2, thetemperatures may be set to the minimum (2° C.) and maximum temperatures(32° C.) specified in any of the three preliminary temperature intervalsin Table 2. The initial temperature T₁ may be representative of theexpected cold storage temperature of the calibration solutions, and theend temperature T₂ may be representative of the temperature thecalibration solutions are expected to experience during transportationand/or during use. As such, the initial temperature and end temperaturemay not be the actual temperature at the initial time t₁ and end timet_(age) respectively.

The parameter t₁ is an unknown amount of time spent at the temperatureT₁. The parameter t_(age) is the age of the solution pack relative tothe time point t=0 when the analyte levels (cCr_(Cal2) ⁰, cCrn_(Cal2) ⁰,cCr_(Cal3) ⁰, cCr_(Cal3) ⁰) in the calibrators are measured using areference method. The analyte levels and the absolute time point atwhich they were measured may be stored electronically in each individualsolution pack and so that they can be easily input upon analysis.

At step 330, the combination of the rate equation 310 (Equation 5), theArrhenius equation 311 (Equation 4) and the temperature model 320 issolved analytically. This is done by solving the resultant differentialequation twice, i.e., in segments of constant temperatures T₁ and T₂with corresponding time spans t₁ and t₂=t_(age)−t₁, respectively, and byusing the appropriate starting conditions in each segment. This leads tothe following equations for the Cr and Crn concentrations in a givencalibrator (“Cal#”) as function of t₁:

$\begin{matrix}{{{cCr}_{{Cal}\mspace{11mu} \#}^{model}( {{t_{1};t_{age}},T_{1},T_{2}} )} = {{\frac{k_{1}( T_{2} )}{K( T_{2} )} \cdot c_{{Cal}\mspace{14mu} \#}^{tot}} + {( {{( {\frac{k_{2}( T_{1} )}{K( T_{1} )} - \frac{k_{2}( T_{2} )}{K( T_{2} )}} ) \cdot c_{{Cal}\mspace{11mu} \#}^{tot}} - {( {{cCr}_{{Cal}\mspace{11mu} \#}^{0} - {\frac{k_{1}( T_{1} )}{K( T_{1} )} \cdot c_{{Cal}\mspace{11mu} \#}^{tot}}} ) \cdot e^{{- t_{1}}{K{(T_{1})}}}}} ) \cdot e^{{- {({t_{age} - t_{1}})}}{K{(T_{2})}}}}}} & {{Equation}\mspace{14mu} 7} \\{{{cCrn}_{{Cal}\mspace{11mu} \#}^{model}( {{t_{1};t_{age}},T_{1},T_{2}} )} = {{\frac{k_{2}( T_{2} )}{K( T_{2} )} \cdot c_{{Cal}\mspace{14mu} \#}^{tot}} + {( {{( {\frac{k_{2}( T_{1} )}{K( T_{1} )} - \frac{k_{2}( T_{2} )}{K( T_{2} )}} ) \cdot c_{{Cal}\mspace{11mu} \#}^{tot}} - {( {{cCrn}_{{Cal}\mspace{11mu} \#}^{0} - {\frac{k_{2}( T_{1} )}{K( T_{1} )} \cdot c_{{Cal}\mspace{11mu} \#}^{tot}}} ) \cdot e^{{- t_{1}}{K{(T_{1})}}}}} ) \cdot e^{{- {({t_{age} - t_{1}})}}{K{(T_{2})}}}}}} & {{Equation}\mspace{14mu} 8}\end{matrix}$

Where c_(Cal#) ^(tot)=cCr_(Cat#) ⁰+cCrn_(Cal#) ⁰ and K(T)=k₁(T)+k₂(T)are constants. Equation 7 gives the concentration of Cr at end timet_(age). Many of the parameters 340 of the Equations 7 and 8 are alreadyknown, and the unknown variable is t₁. The values k₁, k₂ and K can bedetermined from the Arrhenius equations, where α and β are well valuesthat are known to a high accuracy. The concentrations cCr_(Cal#) ⁰,cCrn_(Cal#) ⁰ and c_(Cal#) ^(tot) are the known concentrations frommeasuring the solutions at time t=0. Temperatures T₁ and T₂ and knownfrom the temperature-model used, and t_(age) is known from being thetime since production of the calibration solutions. Therefore, Equations7 and 8 are the expressions at step 331, but before the actualconcentrations can be calculated, the unknown variable t₁ needs to bedetermined from the steps in box 350.

From the sensor response model 351 in Equation 1, the followinguniversally valid relationship can readily be derived for measurementswith the uncalibrated Crea A sensor on both calibrators at a given time,e.g. t=t_(age):

$\begin{matrix}{\frac{I_{{Cal}\; 2}^{A}( t_{age} )}{{cCr}_{{Cal}\; 2}( t_{age} )} = \frac{I_{{Cal}\; 3}^{A}( t_{age} )}{{cCr}_{{Cal}\; 3}( t_{age} )}} & {{Equation}\mspace{14mu} 9}\end{matrix}$

The relationship of Equation 9 is valid for an uncalibrated Crea Asensor as no calibration parameters, i.e. the Cr sensitivity S_(Cr)^(A), enter the equation. Equation 9 states that the ratio between theCrea A sensor signal and the Cr concentration measured for onecalibration solution has the same value as for the other calibrationsolutions at a given time.

The analytical expression for cCr_(Cal#) ^(model) and cCrn_(Cal#)^(model) in Equations 7 and 8 can now be inserted into Equation 9 toform the “Cr-identity” 332 Equation 10.

$\begin{matrix}{\frac{I_{{Cal}\; 2}^{A}( t_{age} )}{I_{{Cal}\; 3}^{A}( t_{age} )} = \frac{{cCr}_{{Cal}\mspace{11mu} 2}^{model}( {{t_{1};t_{age}},T_{1},T_{2}} )}{{cCr}_{{Cal}\mspace{11mu} 3}^{model}( {{t_{1};t_{age}},T_{1},T_{2}} )}} & {{Equation}\mspace{14mu} 10}\end{matrix}$

The raw outputs of the Crea A sensor for the two calibration solutionsat the end time can be input into the left-hand side of Equation 10. Theright-hand side of the equation is a non-linear function of the oneremaining unknown variable t₁, and is a monotonic function within mostrealistic temperature and time ranges. As a monotonic function, only onesolution for t₁ exists, so Equation 10 can be solved by numericalmethods to find t₁ at step 333. As a result, the ratio between the rawsignals of the Crea A sensor leads to one possible value of t₁, andhence one possible temperature profile approximating the truetemperature profile.

Once the value of t₁, and consequently the temperature model, are knownEquations 7 and 8 for the concentrations of the calibration solutionscan be solved 334. Specifically, the Cr concentrations cCr_(Cal2) andcCr_(Cal3), and the Crn concentrations cCrn_(Cal2) and cCrn_(Cal3) canbe determined for the calibration solutions at the end time.

Once the concentrations of Cr and Crn have been estimated for thecalibration solutions at the end time, it is possible to compare theseconcentrations with raw sensor readings of the calibrations solutions todetermine the sensitivities, and hence calibrate 360, the sensors.

Equations 1 and 2 provide the sensor response models for the Crea A andCrea B sensors respectively. At step 361 these sensor response modelscan be used to derive the following relationships:

$\begin{matrix}{S_{Cr}^{A} = \frac{I_{{Cal}\; 3}^{A}}{{cCr}_{{Cal}\; 3}}} & {{Equation}\mspace{14mu} 11} \\{S_{Cr}^{B} = \frac{{I_{{Cal}\; 2}^{B} \cdot {cCrn}_{{Cal}\; 3}} - {I_{{Cal}\; 3}^{B} \cdot {cCrn}_{{Cal}\; 2}}}{{{cCr}_{{Cal}\; 2} \cdot {cCrn}_{{Cal}\; 3}} - {{cCrn}_{{Cal}\; 3} \cdot {cCrn}_{{Cal}\; 2}}}} & {{Equation}\mspace{14mu} 12} \\{S_{Crn}^{B} = \frac{{I_{{Cal}\; 3}^{B} \cdot {cCr}_{{Cal}\; 2}} - {I_{{Cal}\; 2}^{B} \cdot {cCr}_{{Cal}\; 3}}}{{{cCr}_{{Cal}\; 2} \cdot {cCrn}_{{Cal}\; 3}} - {{cCr}_{{Cal}\; 3} \cdot {cCrn}_{{Cal}\; 2}}}} & {{Equation}\mspace{14mu} 13}\end{matrix}$

The calibration concentrations can be determined from step 334, and theraw signals for the Crea A sensor at Cal3 and the Crea B sensor at Cal2and Cal3 can be determined at step 362. These values can be substitutedinto Equations 11, 12 and 13 at step 363 to calculate the sensitivitiesof the Crea A sensor for Cr, and the Crea B sensor for Cr and Crn. Withthese sensitivities, it is possible to accurately measure theconcentrations of Cr or Crn in any given sample.

While FIG. 3 outlines the steps for deriving the proposed method, FIG. 4summarises the steps for carrying out an example embodiment of theproposed method. The proposed method is not limited to the ordering ofthe steps shown in FIG. 4, nor is the method envisioned to be solelylimited to this example embodiment provided.

At step 410, the concentrations of the Cr and Crn in the calibrationsolutions are measured and recorded at an initial time. The initial timemay be just after production of the solutions and/or at any appropriatetime before dispatch of the calibration solutions. The concentrationsmay be measured using a range of techniques and known sensors, such asby high-performance liquid chromatography (HPLC). The concentrations maybe recorded by any means that allow the end user to use these recordedconcentrations in the subsequent calculations. For example, theconcentrations may be stored in writing on the calibration pack, or maybe stored electronically at a server, or may be stored electronically atthe calibration pack itself so that a calibration machine canautomatically read the stored variable. Similarly, the packs may betime-stamped so that the initial time will be known when performing thesubsequent calculations.

At step 420 the calibration solutions are dispatched to the endconsumer. From this point, the actual temperatures the calibrationsolutions are stored at may not be known.

Box 430 illustrates the steps that can be taken by an end userattempting to calibrate the Cr and Crn sensors, starting with receivingthe calibration solutions and starting the calibration process at an endtime (also referred to as t_(age)) 440.

At step 450, the raw Cr and Crn signals in the calibration solutions aremeasured by the sensors. These raw signals are the current outputsI_(Cal2) ^(A)(t_(age)), I_(Cal3) ^(A)(t_(age)), I_(Cal2) ^(B)(t_(age))and I_(Cal3) ^(B)(t_(age)) of the sensors.

At step 460, the temperature model is determined. In the example of atwo-temperature model, this involves calculating the intermediate timet₁ by solving Equation 10 for t₁. To perform this calculation, theArrhenius values for the relevant reactions need to be known, along withthe initial time and initial concentrations that were recorded at step410.

At step 470, the actual concentrations of Cr and Crn in the calibrationsolutions are calculated by solving Equations 7 and 8 using thetemperature model determined at step 460.

At step 480, the sensor outputs calculated in step 450 (specifically,I_(Cal3) ^(A)(t_(age)), I_(Cal2) ^(B)(t_(age)) and I_(Cal3)^(B)(t_(age))) and the concentrations calculated at step 470 aresubstituted into Equations 11 to 13 to determine the sensorsensitivities, thereby calibrating the sensors.

The steps performed at box 430 may be performed manually by an end user.Alternatively, some or all of the steps at box 430 can be automated by asystem. For example, a calibration system may take the calibration packand automatically read electronic data indicating the initialconcentrations and initial time. The calibration system may measure allthe raw sensor outputs as indicated in steps 450 and 470. Thecalibration system may contain an electronic device with a processor forperforming the calculations of steps 460, 470 and 480. Computer softwaremay be supplied in a computer-readable medium that the user can installon their own computer to automatically perform any of the calculationsof the method.

While the temperature model used to calibrate the sensors is only anestimation of the true temperature profile of the calibration solutions,the proposed solution provides very accurate results. FIG. 5 shows anumber of graphs comparing the actual concentrations of the calibrationsolutions (using HPLC, for example) with the concentrations calculatedwith the proposed method.

The tests were performed for Cal2 and Cal3 solutions stored at differenttemperatures for a variety of time spans, which correspond to realistictime/temperature scenarios for the solution packs, but also to extremescenarios which exceed the specified time/temperature ranges in Table 1.

Data points 511, 521, 531 and 541 are for calibration solutions storedat 10° C. for 53 days. Data points 512, 522, 532 and 542 are forcalibration solutions stored for 53 days at 10° C., 15 days at 32° C.,and 34 days at 10° C. Data points 513, 523, 533 and 543 are forcalibration solutions stored for 53 days at 10° C., 15 days at 6° C., 29days at 10° C., and 20 days at 6° C. Data points 514, 524, 534 and 544are for calibration solutions stored for 53 days at 10° C., 15 days at25° C., 29 days at 10° C., and 20 days at 25° C. Data points 515, 525,535 and 545 are for calibration solutions stored for 53 days at 10° C.,32 days at 32° C., 29 days at 10° C., and 20 days at 32° C.

Graph 510 shows the calculated and actual Cr concentrations in the Cal2solution at different temperature conditions. The linear trendline 516(formula y=1.0317x+2.0703) indicates a linear relationship between thecalculated and actual concentrations, with an R² value of 0.98. Graph520 shows the calculated and actual Crn concentrations in the Cal2solution at different temperature conditions. The linear trendline 526(formula y=0.9466x+24.0) indicates a linear relationship between thecalculated and actual concentrations, with an R² value of 0.9786. Graph530 shows the calculated and actual Cr concentrations in the Cal3solution at different temperature conditions. The linear trendline 536(formula y=0.9522x+17.951) indicates a linear relationship between thecalculated and actual concentrations, with an R² value of 0.97. Graph540 shows the calculated and actual Crn concentrations in the Cal3solution at different temperature conditions. The linear trendline 546(formula y=0.9621x+5.5329) indicates a linear relationship between thecalculated and actual concentrations, with an R² value of 0.97.

These graphs show that even though the temperature model is only anestimate of the true temperature profile, the concentrations calculatedwith the proposed method are consistently close to the actualconcentrations.

FIG. 6 shows a number of graphs comparing the actual concentrations ofthe calibration solutions (using HPLC, for example) with theconcentrations calculated with the example embodiment using atemperature logger to generate a temperature model.

The tests were performed for Cal2 and Cal3 solutions stored at differenttemperatures for a variety of time spans, which correspond to realistictime/temperature scenarios for the solution packs, but also to extremescenarios which exceed the specified time/temperature ranges in Table 1.

Graph 610 shows the calculated Cr concentrations in the Cal2 solutioncompared to the actual concentrations. The linear trendline 611 (formulay=1.0395x−0.24446) indicates a linear relationship between thecalculated and actual concentrations, with an R² value of 0.9899. Graph620 shows the calculated Crn concentrations in the Cal2 solutioncompared to the actual concentrations. The linear trendline 621 (formulay=0.9681x+15.401) indicates a linear relationship between the calculatedand actual concentrations, with an R² value of 0.992. Graph 630 showsthe calculated Cr concentrations in the Cal3 solution compared to theactual concentrations. The linear trendline 631 (formulay=0.931x+32.896) indicates a linear relationship between the calculatedand actual concentrations, with an R² value of 0.9656. Graph 640 showsthe calculated Crn concentrations in the Cal3 solution compared to theactual concentrations. The linear trendline 641 (formulay=0.9465x+1.5862) indicates a linear relationship between the calculatedand actual concentrations, with an R² value of 0.9707.

These graphs show that using temperature probes to record historicchanges in temperature can lead to very accurate calculations for Crand/or Crn concentrations.

It is to be understood that the present disclosure includes permutationsof combinations of the optional features set out in the embodimentsdescribed above. In particular, it is to be understood that the featuresset out in the appended dependent claims are disclosed in combinationwith any other relevant independent claims that may be provided, andthat this disclosure is not limited to only the combination of thefeatures of those dependent claims with the independent claim from whichthey originally depend.

1. A method for calibrating a device for measuring the concentration ofcreatinine using one or more calibration solutions, the methodcomprising: receiving concentrations at an initial time of creatine, Cr,and/or creatinine, Crn, of the one or more calibration solutions;receiving outputs of the measuring device at an end time; calculatingthe concentration of Cr and/or Crn in the calibration solutions at anend time using a temperature model, wherein the temperature modelindicates changes in temperature of the calibration solutions from theinitial time to the end time; and determining a relationship between theoutputs of the measuring device and the calculated concentrations of Crand/or Crn.
 2. The method of claim 1, wherein the measuring deviceincludes a sensor for measuring creatine in one or more of thecalibration solutions.
 3. The method of claim 1, wherein the measuringdevice includes a sensor for measuring creatinine in one or more of thecalibration solutions.
 4. The method of claim 1, wherein the measuringdevice includes a sensor for measuring creatine and creatinine in one ormore of the calibration solutions.
 5. The method of claim 1, wherein themeasuring device is an amperometric measuring device.
 6. The method ofclaim 1, further comprising determining the temperature model byreceiving measurements of the changes in temperature of the calibrationsolutions from a temperature probe from the initial time to the endtime.
 7. The method of claim 6, wherein said received measurements arerecorded measurements.
 8. The method of claim 6, wherein saiddetermining the temperature model comprises calibrating the receivedmeasurements of the changes in temperature with a second temperatureprobe.
 9. The method of claim 1, wherein the determining a relationshipbetween the measuring device outputs and the calculated concentrationsof Cr and Crn comprises calculating sensor sensitivities of themeasuring devices.
 10. The method of claim 9, further comprisingreceiving temperature measurements after the end time and updating thecalculated sensitivities of the measuring devices using the temperaturemeasurements received after the end time.
 11. The method of claim 1,wherein the end time is greater than 14 days after the initial time. 12.A computer readable medium comprising instructions which when executedby one or more processors of an electronic device, cause the electronicdevice to operate in accordance with the method as claimed in claim 1.13. An electronic device comprising: one or more processors; and memorycomprising instructions which when executed by one or more of the one ormore processors cause the electronic device to operate in accordancewith the method claimed in claim
 1. 14. A package comprising one or morecalibration solutions, the package containing instructions for use withthe method of claim
 1. 15. The package of claim 14 further comprising anindication of the initial time and the concentrations at the initialtime of Cr and/or Crn of the one or more calibration solutions.
 16. Thepackage of claim 14, further comprising a temperature probe formeasuring the temperatures of the creatinine solutions from the initialtime to the end time, and memory for storing the measured temperatures.17. A package comprising one or more calibration solutions, the packagecontaining instructions for use with the electronic device of claim 13.18. The package of claim 17, further comprising an indication of theinitial time and the concentrations at the initial time of Cr and/or Crnof the one or more calibration solutions.
 19. The package of claim 17,further comprising a temperature probe for measuring the temperatures ofthe creatinine solutions from the initial time to the end time, andmemory for storing the measured temperatures.